Method for the treatment of industrial waste

Patent metadata

Field	Value
Publication number	US-10227246-B2
Application number	US-201213591695-A
Country	US
Kind code	B2
Filing date	Aug 22, 2012
Priority date	Feb 25, 2010
Publication date	Mar 12, 2019
Grant date	Mar 12, 2019

Abstract

There is provided a method for treating spent metal working fluid (MWF), comprising the steps of: (a) providing a biofilm of microorganisms on a solid support matrix in a first bioreactor; (b) transferring at least a portion of the solid support matrix comprising the biofilm of microorganisms from the first bioreactor into a second bioreactor; and (c) incubating the microorganisms in the second bioreactor to reduce the chemical oxygen demand of the spent MWF contained therein.

First claim

The invention claimed is:

1. A method for treating spent metal working fluid (MWF) by reducing chemical oxygen demand (COD) content in the MWF, comprising the steps of:
(a) providing a mature biofilm of microorganisms on a solid support matrix in a first bioreactor, wherein the mature biofilm is capable of reducing the chemical oxygen demand (COD) of spent MWF to 2000 mg/L or less in 30 days or less;
(b) transferring the solid support matrix comprising the mature biofilm of microorganisms from the first bioreactor into a second bioreactor;
(c) incubating the second solid support matrix comprising the mature biofilm of microorganisms from step (b) in the second bioreactor to reduce the chemical oxygen demand (COD) of a diluted spent MWF contained therein; and
(d) increasing the concentration of the diluted spent MWF obtained in step (c) so as to increase the chemical oxygen demand (COD) of the fluid contained in the second bioreactor.

2. The method according to claim 1 , wherein the mature biofilm of microorganisms on the solid support matrix is capable of reducing the COD of spent MWF to 2000 mg/L or less prior to being transferred to the second bioreactor.

3. The method according to claim 1 , wherein the volume of the first solid support matrix comprising the mature biofilm of microorganisms that is transferred from the first bioreactor into the second bioreactor in step (b) is at least about 10% of the volume of the second bioreactor.

4. The method according to claim 3 , wherein the remaining volume of the second bioreactor is occupied by a solid support matrix upon which a biofilm of microorganisms is not or is not substantially present.

5. The method according to claim 1 , wherein the second bioreactor is initially filled either before or after step (b) with spent MWF, suitably, diluted spent MWF, in which the COD thereof is between about 5,000 to about 10,000 mg/L.

6. The method according to claim 1 , wherein the solid support matrix comprises, consists or consists essentially of woven tubes of plastic.

7. The method according to claim 1 , wherein air flow in the first and/or the second bioreactor is between about 250 to 300 liters per minute per 5000 liters of liquid bioreactor volume at a temperature from about 1 to 35° C.

8. The method according to claim 1 , wherein the mature biofilm that is established in step (a) is: (i) derived from an indigenous community of microorganisms isolated from MWF; or (ii) a biofilm derived from a different bioreactor which has been inoculated by transferring at least a portion of a solid support matrix comprising a mature biofilm of microorganisms, and wherein said bioreactor is able to reduce the COD of spent MWF to 2000 mg/L.

9. The method according claim 1 , wherein at least a portion of the spent MWF from the second bioreactor is used to inoculate one or more further bioreactors, optionally wherein the further bioreactor(s) comprise a solid support matrix which is not substantially colonised by microorganisms.

10. The method according to claim 9 , where said step is repeated one or more times to inoculate one or more further bioreactors.

11. A method for preparing a biofilm of microorganisms that is capable of reducing the COD content of spent MWF comprising the steps of:
(a) providing a mature biofilm of microorganisms on a solid support matrix in a first bioreactor, wherein the mature biofilm is capable of reducing the chemical oxygen demand (COD) of spent MWF to 3000 mg/L or less in 30 days or less;
(b) transferring the solid support matrix comprising the mature biofilm of microorganisms from the first bioreactor into a second bioreactor;
(c) culturing the biofilm of microorganisms in the second bioreactor in the presence of a diluted spent MWF; and
(d) increasing the concentration of the diluted spent MWF obtained in step (c) so as to increase the chemical oxygen demand of the fluid contained in the second bioreactor.

12. A method for treating spent metal working fluid (MWF), comprising the steps of:
(a) providing a mature biofilm of microorganisms on a solid support matrix in a first bioreactor, wherein the mature biofilm is capable of reducing the chemical oxygen demand (COD) of spent MWF to 2000 mg/L or less in 30 days or less;
(b) transferring the solid support matrix comprising the mature biofilm of microorganisms from the first bioreactor into a second bioreactor;
(c) incubating the second solid support matrix comprising the mature biofilm of microorganisms from step (b) in the second bioreactor to reduce the chemical oxygen demand of a diluted MWF contained therein; and
(d) increasing the concentration of the diluted spent MWF obtained in step (c) so as to increase the chemical oxygen demand of the fluid contained in the second bioreactor.

13. A method of maturing a bioreactor for treating spent metal working fluid (MWF), the method comprising
a) inoculating the bioreactor by solid matrix inoculation with a biofilm of two or more species of microorganisms on a solid support matrix, the biofilm having matured in and been transferred from a different bioreactor and is capable of reducing the chemical oxygen demand (COD) of spent MWF, and
b) incubating with diluted spent MWF, and
c) incubating with diluted spent MWF obtained in step (b) of increasing concentration so as to increase the COD of the fluid contained in the bioreactor,
thereby maturing the bioreactor within about 30 days or less.

14. The method of claim 13 , wherein the volume of solid support matrix with biofilm transferred into the bioreactor is at least 10%, 15% or 20% or more of the volume of the bioreactor.

15. The method of claim 13 , wherein the solid support matrix comprises woven tubes of plastic.

16. The method of claim 13 , wherein the biofilm is capable of reducing the COD content of spent MWF to about 2000 mg/L or less.

17. The method of claim 13 , wherein maturing the bioreactor occurs at from about 12° C. to about 20° C.

18. The method of claim 13 , wherein the bioreactor is aerated following inoculation.

Assignees

• Ager Duane
• Goodall Timothy
• Pope William
• Ford Motor Co

Inventors

• Ager Duane
• Goodall Timothy
• Pope William

Classifications

• C02F3/348

  characterised by the way or the form in which the microorganisms are added or dosed · CPC title

• C02F2103/16

  from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes · CPC title

• C02F3/34 Primary

  characterised by the microorganisms used · CPC title

• C02F3/02 Primary

  Aerobic processes · CPC title

• C02F3/103 Primary

  Textile-type packing · CPC title